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JPH0229601B2 - SANSOFUKAKI - Google Patents

SANSOFUKAKI

Info

Publication number
JPH0229601B2
JPH0229601B2 JP59054405A JP5440584A JPH0229601B2 JP H0229601 B2 JPH0229601 B2 JP H0229601B2 JP 59054405 A JP59054405 A JP 59054405A JP 5440584 A JP5440584 A JP 5440584A JP H0229601 B2 JPH0229601 B2 JP H0229601B2
Authority
JP
Japan
Prior art keywords
atmospheric
enricher
atmosphere
passage
oxygen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59054405A
Other languages
Japanese (ja)
Other versions
JPS60200804A (en
Inventor
Tsuguyasu Shimote
Toshio Motoki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Teijin Ltd
Original Assignee
Teijin Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Teijin Ltd filed Critical Teijin Ltd
Priority to JP59054405A priority Critical patent/JPH0229601B2/en
Publication of JPS60200804A publication Critical patent/JPS60200804A/en
Publication of JPH0229601B2 publication Critical patent/JPH0229601B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Description

【発明の詳細な説明】 a 産業上の利用分野 本発明は大気から酸素の豊富な空気を安定して
効率よく得る装置に関するものであり、特に医療
用に使用するに適した酸素富化器に関する。 近年喘息、肺気腫症、慢性気管支炎等の呼吸気
系器管の疾患に苦しむ患者が多く、その最も効果
的な治療法の1つとして酸素吸入法がある。この
酸素吸入法の酸素源としては現在の多くは深冷分
離法によつて得た純酸素をボンベ等に詰め供給す
る方法あるいは液化酸素を直接蒸発させて配管に
より供給する方法がとられているが、酸素切れの
監視、高圧ガスとなつている純酸素ガスによる火
気管理の複雑さ・厳しさ、あるいは高圧ガスボン
ベの取扱い等管理の厳しさが要求され、ボンベの
取換えや運搬に煩雑さを伴なう、配管による場合
は複雑な設備・経路及び高い設置費が必要となる
等により、この方式は特に一般家庭内で使用する
のは困難である。 一方患者のすぐ近くで大気中の酸素を分離・濃
縮する酸素富化器が簡便な酸素供給源として注目
されてきている。この様な酸素富化器は、酸素よ
り窒素をより選択的に吸着するゼオライト等の吸
着剤を用いた吸着分離法と、窒素より大きい速度
で酸素を透過させることが出来る選択性透過膜を
用いた膜分離法との大別して2種類ある。 本発明は上述の如きの酸素富化器での、特に患
者近くで使用する際最も問題となる騒音につき改
良を加えたものである。 b 従来技術 上述の酸素富化器は吸着分離法、膜分離法のい
ずれに於ても、電動機の動力によりポンプを駆動
せしめて、吸着分離法では大気を1〜3Kg/cm2
に圧縮して吸着剤に接触させ窒素を吸着させ、膜
分離法では選択性透過膜を通過した酸素成分の多
いガスを100〜300Torrの真空状態に維持して所
定の酸素濃度を得る構成をとつている。 連続的に酸素成分の濃縮された空気(以下富化
空気と略称する)を得るために、吸着分離法では
吸着剤に空気を吸着および離脱させる必要から操
作圧力は加圧および/又は減圧を繰返す、いわゆ
るプレツシヤー・スイング方式であり、圧縮機に
よる騒音が大きくその騒音が大きくなつたり小さ
くなつたりの繰返しで使用者、特に病人にとつて
苦痛を感じさせる。膜分離法は生成された富化空
気を真空にするのみでかつ圧力(真空度)も一定
であるため吸着分離法に比し、真空ポンプより発
生する騒音はかなり低位にあるが、夜間等の周囲
の騒音レベルが低い場合特に睡眠時には患者ある
いは周辺に在居する人にとつては苦痛を感じさせ
る。 現在迄の酸素富化器は富化空気性状の高度化あ
るいは酸素富化器の小型化に技術の焦点があてら
れ、使用者の立場にたつての騒音対策を深く検討
するに到つていない。 酸素富化器に於ては電動機の動力によりポンプ
手段を駆動せしめているため電動機を冷却するこ
と、ガスを圧縮する(吸着分離法では大気を、膜
分離法では富化空気を真空から大気圧迄夫々圧縮
する。)ために発生するポンプ自体の昇温を極力
防止することが、酸素富化器を安定して効率よく
作動させる必須要件である。従つて、一般には富
化空気の数倍乃至数10倍り多量の空気を冷却フア
ンを介して電動機及びポンプに接触させてこれら
を冷却させる方策を採つている。このため酸素富
化器には冷却用の大気の通路として、その外壁に
は大気を流入出させるための面積の大きな開口部
を、その内部には大きな空間をもつ流路が設置さ
れている。 一方酸素富化器における騒音の発生ポンプ、電
動機及び冷却フアンが主たるもので、更に吸着分
離法ではプレツシヤー・スイングで吸着剤を再生
する時にに吸着剤に吸着された窒素成分の多い空
気を除圧して離脱させて大気に排出させる際の排
出音を瞬時的ではあるが割合大きなものである。 騒音を低位に保つためには騒音の発生源を密閉
した空間に設置するのが最も簡便で確実な方法で
あるが、上述の説明で明らかなように各部位の冷
却のための大気の通路を確保する必要上から上記
の方策の採用は難しい。 c 発明の目的 本発明は上記の点を鋭意研究し、特に騒音発生
源から酸素富化器外壁に設けられた開口部迄の冷
却風の通る距離及び騒音発生源周りの周壁に生ず
る壁面振動に着目してなされたもので、騒音レベ
ルの低位な酸素富化器、特に医療用に好適な酸素
富化器を提供することを目的とする。 d 発明の構成 電動機の動力により駆動せめるポンプ手段を少
なくとも1個使用して大気より酸素富化空気を得
る酸素富化器において、該富化器の外殻を形成す
る面に設けられた大気取入口及び大気排出口と、
該富化器に内蔵された該電動機及び該ポンプ手段
を収納する室構造であつて該室構造を形成する面
に設けられた該室構造への大気流入開口部及び該
室構造からの大気流出開口部を有する少なくとも
1個のポンプ収納室と、該大気取入口から該大気
流入開口部への大気の流れを拘束する大気流入通
路と、該大気流出開口部から該大気排出口への大
気の流れを拘束する大気排出通路とを有し、該大
気流入通路の長さと該大気排出通路の長さの各々
が該富化器外殻を構成する面における相対する両
端間の長さの最小値以上であり、該大気流入通路
と該大気排出通路の各々の屈曲回数が3回以上と
なるように構成されていることを特徴とする酸素
富化器及びさらに該富化器の前面側の外殻の内側
の少なくとも一部に空間部を有することを特徴と
する酸素富化器である。 本願発明における酸素富化器は、大気より酸素
濃度の高められたいわゆる酸素富化空気を得るも
のであり、その酸素濃度を高める手段としては吸
着分離、膜分離手段のいずれを用いてもよい。ま
た該酸素富化器は、電動機の動力により駆動され
るポンプ手段、すなわち真空ポンプ、圧縮機等を
少なくとも1個内蔵するものである。かかるポン
プ手段は該富化器の1部を構成するポンプ収納室
に収納されるが、該収納室には1個又は2個以上
のポンプ手段を収納することができ、該収納室は
通常1個が好ましいが、2個以上であつてもよ
い。尚該富化器内で用いられる送風機は大気通路
の途中にあつてもよいが、発生する騒音が大きい
場合には該収納室に内蔵せしめることが可能であ
る。 本発明の酸素富化器内を流れる大気とは、該ポ
ンプ手段等に連結されたポンプ内を流れる空気で
はなくて、ダクト等の比較的大きな通路を流れる
空気を意味するものである。 本発明にかゝる酸素富化器を用いて更に詳しく
説明するが、該図面は本発明の一実施態様に示す
にすぎず、本発明は図面により制限を受けるもの
ではない。 第1図は本発明を適用した膜分離法酸素富化器
(以下膜型富化器と略す)の概略構造を示す。 膜型富化器に於ては分離膜の片側に多量の大気
を掃引させ、他方を低位に保つと分離膜のガスの
選択透過性により低圧側に酸素が濃縮(富化)さ
れる。この様な分離膜を多数杖積層し実用的な形
としたものをモジユールと言う。 図に於て、筐体1は多数の壁部材により大気の
通路が構成され、大気取入口2により筐体外から
取り入れられた大気は送風機3、膜モジユール4
を含む大気流入通路5を通つて真空ポンプ6が設
置された収納室7の大気流入開口部8を通つて収
納室内に送りこまれる。収納室7の中で、真空ポ
ンプ6のポンプ部及びモータと熱交換し、温めら
れた大気は大気流出開口部9より収納室7から排
出され、大気排出通路10を経て大気排出口11
より筐体外へ排出される。 以上の大気通過経路の中で、最も騒音レベルの
高い部位はポンプの収納室7で、この収納室7よ
り発生する騒音をいかに抑制しあるいは筐体外へ
伝播させないかが技術上の要点となる。尚送風機
からの騒音は小さいので、ここでは無視して前記
の如く大気流入通路の一部と考える。 収納室7の騒音レベルを低下させるためには、
低騒音型の真空ポンプを使用するとか、収納室7
内にに吸音材を設置するとかの手段がとられる
が、かゝる手段のみでは現在要求される医療用酸
素富化器の騒音レベルを満足しえず、収納室7か
らの音の伝播抑制に工夫が必要となる。この一手
段として収納室7内に吸音材に加えて遮音材を設
置する事も考えられ、これにより収納室7から壁
面を通じての音の伝播はかなり抑制されるが、真
空ポンプ冷却に必要な空気量が多いため大気流入
開口部8及び大気流出開口部9の面積を小さくす
るにも限度がありこの部分からの音の漏出が相当
高レベルとなりこの騒音を如何に抑制するかが富
化器全体の騒音レベルの高低を左右してくる。膜
型富化器に於ては第1図にもみられるように膜モ
ジユール4等が大気流入量路に設置され、又経路
も相当屈曲せしめられる構造としうるので、大気
流入開口部8からの漏出騒音は大気取入口2に達
する迄に相当減衰し、大気流出開口部9からの漏
出騒音が支配的となる。 本発明者らは上記漏出騒音を低位に抑えるべく
鋭意検討の結果、収納室7に設けられた開口部8
又は9から筐体の開口部2又は11迄の通路長、
即ち2→8の通路長及び9→11の通路長の各々
を富化器外殻面の寸法の最小値よりも大きくとり
かつ通路の屈曲回数を少なくとも3回以上とると
漏出騒音を非常に減衰させうる事が判明し、本発
明に到達したものである。 大気の通過距離を長くすればするほどその長さ
に応じて騒音レベルは一般に低下するが富化器の
如く種々の周波数が混在する騒音では余程注意し
て通過距離を選定しないと逆に共鳴により特定周
波数の音が増幅される可能性がある。ところが大
気の通路を適当回屈曲させると通過距離がある一
定長以上であれば共鳴も抑制しうると同時に種々
の周波数の駆音をほゞ均等に低減しうる事がわか
つた。即ち通過距離としては富化器の外殻寸法の
最小値以上、好ましくは1.5倍以上を確保すれば
よい。あまりに通過距離が短かいと低周波数の音
が減衰しない。 一方大気通路の屈曲部での吸音効果の出現音の
反射あるいは音の共鳴防止があり、騒音低減に大
きな効果がみられるが、いたずらに屈曲回数を多
くすることは富化器の構造を複雑とし筐体コスト
を上げることばりでなく、大気の圧力損失も大き
くなり送風機の騒音レベルを上昇させることとな
り好ましい事ではない。屈曲回数は低周波数域迄
有効に騒音レベルを低減させるためには3回以上
が好ましい。更に屈曲部位に吸音材あるいは吸音
材及び遮音材を設置するとより好ましい。一般の
機器に於ける騒音対策は4000Hz程度の高周波数の
騒音を問題とするが、酸素富化器に於ては100〜
2000Hzの周波数が支配的であり、500Hz以下の騒
音レベル低下には上記手段が非常に有効である。 第2図に膜型富化器での大気排出通路の種々の
実施例を示す。第2図に於て、図面の左側が該富
化器の前面側(通常は操作面である)を示し、図
中一点鎖線の途中に丸印を付された部分が本質的
な屈曲部位を示す。大気排出口で屈曲排出される
事は大きな騒音低下とはならないので無視して考
えるのが好ましい。第2図aは第1図の大気通路
を模式的に示したもので、屈曲回数は3回であ
り、b,c,dの側では夫々、4、3、4回であ
る。第2図cに見られるように、操作側の筐体壁
部材12と収納室壁部材13により空間部14を
構成すると、収納室7の周辺より発生する面音が
直接筐体外へ放出されることなく騒音レベル抑制
に非常に有効であり、又該空間部14をaあるい
はb図の様に空気経路の一部として使用すること
は、収納室面音防止及び経路長増加、屈曲数増加
の点からも非常に好ましい。 第2図の一点鎖線で示される空気経路中で屈曲
部に吸音材を設置することが有効な事は前述した
が、より吸音効果を高めるため経路自体にも吸音
材を設置することが好ましく、屈曲部も含めて全
長の1/5以上設置するとより好ましい。 吸着型富化器に於ては膜型の様に多量の掃引大
気は必要としないがポンプ温度上昇が大きいため
結果的には膜型と同程度の冷却空気を必要とす
る。吸着型ではポンプが圧縮機のため発生騒音は
模型より大きく又富化器自体の構造が簡単なため
本発明を適用し冷却空気経路を工夫すれば大きな
騒音レベルの低下が企れる。第3図は本発明の実
施態様を例示する。 第3図aは大気のポンプ収納室7への入、出の
流路の屈曲回数を3回、b,cは各々5回、4回
とした例を示すもので、bは流入側の、cは流出
側の流路を示す。b,cが一体化された場合には
通過部位が重複している部分は紙面垂直方向に流
路が2分割された状態を示し、筐体構造を簡略化
しつゝ通過長の増大及び屈曲回数の増加を企つた
ものである。 e 発明の効果 本発明によつて、酸素富化器からの漏出騒音を
減衰せしめることができ、極めて静かな運転が可
能な酸素富化器を提供することが可能である。 その実施例として、膜型富化器で第4図に示す
屈曲回数2回のもの、第2図cの3回のもの、第
第2図bの4回のものについて騒音低下効果を測
定した結果を次表に示す。 尚、静粛感が出るのは該騒音低下効果が15dB
(A)以上であるとされている。 【表】
DETAILED DESCRIPTION OF THE INVENTION [a] Industrial Application Field The present invention relates to a device for stably and efficiently obtaining oxygen-rich air from the atmosphere, and particularly relates to an oxygen enricher suitable for medical use. . BACKGROUND OF THE INVENTION In recent years, many patients are suffering from diseases of the respiratory system such as asthma, emphysema, and chronic bronchitis, and oxygen inhalation is one of the most effective treatments for these diseases. Most current oxygen sources for this oxygen inhalation method include supplying pure oxygen obtained by cryogenic separation into cylinders, or directly evaporating liquefied oxygen and supplying it through piping. However, it requires monitoring for oxygen exhaustion, the complexity and severity of fire control due to high-pressure pure oxygen gas, and the strict management of handling high-pressure gas cylinders, making replacing and transporting cylinders complicated. This method is particularly difficult to use in general homes because piping requires complicated equipment and routes and high installation costs. On the other hand, oxygen enrichers that separate and concentrate atmospheric oxygen in close proximity to patients are attracting attention as a simple oxygen supply source. This type of oxygen enricher uses an adsorption separation method using an adsorbent such as zeolite, which adsorbs nitrogen more selectively than oxygen, and a selective permeation membrane, which allows oxygen to permeate at a higher rate than nitrogen. There are two main types of membrane separation methods. The present invention improves the noise that is most problematic in the oxygen enricher as described above, especially when it is used near a patient. b Prior art In both the adsorption separation method and the membrane separation method, the above-mentioned oxygen enricher uses the power of an electric motor to drive the pump, and in the adsorption separation method, the atmospheric air is 1 to 3 kg/cm 2 G.
In the membrane separation method, the oxygen-rich gas that has passed through the selectively permeable membrane is maintained in a vacuum state of 100 to 300 Torr to obtain a predetermined oxygen concentration. It's on. In order to continuously obtain air enriched with oxygen components (hereinafter referred to as enriched air), the adsorption separation method requires air to be adsorbed and desorbed by the adsorbent, so the operating pressure is repeatedly increased and/or depressurized. This is the so-called pressure-swing system, and the compressor makes a lot of noise, which repeatedly increases and decreases, causing pain to the user, especially the sick. In the membrane separation method, the generated enriched air is only evacuated and the pressure (degree of vacuum) is also constant, so the noise generated by the vacuum pump is considerably lower than that in the adsorption separation method. When the ambient noise level is low, it can be painful for the patient or people living in the vicinity, especially when sleeping. The technology of oxygen enrichers to date has focused on improving the properties of enriched air or making the oxygen enricher more compact, and it has not been possible to deeply consider noise countermeasures from the user's perspective. . In an oxygen enricher, the pump means is driven by the power of the electric motor, so the electric motor is cooled and the gas is compressed (in the adsorption separation method, the atmosphere is transferred, and in the membrane separation method, the enriched air is transferred from vacuum to atmospheric pressure). It is an essential requirement for the stable and efficient operation of the oxygen enricher to prevent as much as possible the temperature rise of the pump itself, which occurs due to the compression of the oxygen up to the maximum temperature. Therefore, a measure is generally taken in which an amount of air several to several ten times larger than the enriched air is brought into contact with the electric motor and pump via a cooling fan to cool them. For this reason, the oxygen enricher is provided with a large-area opening on its outer wall for air to flow in and out, and a flow path with a large space inside, as a passage for cooling air. On the other hand, the pump, electric motor, and cooling fan are the main sources of noise in the oxygen enricher, and in addition, in the adsorption separation method, when regenerating the adsorbent with a pressure swing, the air rich in nitrogen adsorbed by the adsorbent is depressurized. The sound emitted when the gas is released into the atmosphere is instantaneous, but it is relatively loud. The easiest and surest way to keep noise levels low is to install the noise source in a closed space, but as is clear from the above explanation, it is best to install air passages to cool each part. It is difficult to adopt the above measures due to the need to secure the required amount. c. Purpose of the Invention The present invention has been made by intensively researching the above-mentioned points, and has particularly focused on the distance through which cooling air passes from the noise source to the opening provided in the outer wall of the oxygen enricher, and the wall vibrations that occur on the peripheral wall around the noise source. The object of this invention is to provide an oxygen enricher with a low noise level, particularly an oxygen enricher suitable for medical use. d Structure of the Invention In an oxygen enricher for obtaining oxygen-enriched air from the atmosphere using at least one pump means driven by the power of an electric motor, an air intake provided on a surface forming an outer shell of the enricher is provided. an inlet and an atmospheric outlet;
A chamber structure that houses the electric motor and the pump means built in the enricher, and an air inflow opening into the chamber structure provided on a surface forming the chamber structure, and an air outflow from the chamber structure. at least one pump housing having an opening; an atmospheric inflow passage restricting the flow of atmospheric air from the atmospheric air intake to the atmospheric inlet opening; an atmospheric exhaust passageway that restricts the flow, and the length of the atmospheric inflow passageway and the length of the atmospheric exhaust passageway are each the minimum length between opposite ends of the surface constituting the enricher outer shell. As described above, the oxygen enricher is characterized in that each of the atmospheric inflow passage and the atmospheric discharge passage is bent three times or more, and furthermore, the oxygen enricher is provided with an outer surface on the front side of the oxygen enricher. The oxygen enricher is characterized by having a space at least partially inside the shell. The oxygen enricher according to the present invention obtains so-called oxygen-enriched air having a higher oxygen concentration than the atmosphere, and either adsorption separation or membrane separation may be used as a means for increasing the oxygen concentration. Further, the oxygen enricher incorporates at least one pump means, such as a vacuum pump or a compressor, driven by the power of an electric motor. Such a pump means is housed in a pump storage chamber forming a part of the enricher, but the storage chamber can accommodate one or more pump means, and the storage chamber usually has one or more pump means. It is preferable that the number is 2, but it may be 2 or more. The blower used in the enricher may be placed in the middle of the atmospheric passage, but if the generated noise is large, it may be built in the storage chamber. The atmosphere flowing through the oxygen enricher of the present invention does not mean air flowing through a pump connected to the pump means, but air flowing through a relatively large passage such as a duct. Although the oxygen enricher according to the present invention will be explained in more detail, the drawings merely show one embodiment of the present invention, and the present invention is not limited by the drawings. FIG. 1 shows a schematic structure of a membrane separation method oxygen enricher (hereinafter abbreviated as membrane type enricher) to which the present invention is applied. In a membrane type enricher, by sweeping a large amount of air to one side of the separation membrane and keeping the other side at a low level, oxygen is concentrated (enriched) on the low pressure side due to the gas selective permeability of the separation membrane. A practical configuration in which many such separation membranes are stacked together is called a module. In the figure, a housing 1 has an air passage formed by a large number of wall members, and air taken in from outside the housing through an air intake port 2 is passed through a blower 3 and a membrane module 4.
The air is fed into the storage chamber through the air inflow passage 5 containing the air, and through the air inflow opening 8 of the storage chamber 7 in which the vacuum pump 6 is installed. Inside the storage chamber 7 , heat is exchanged with the pump section and motor of the vacuum pump 6 , and the heated atmosphere is discharged from the storage chamber 7 through the atmosphere outlet opening 9 , passes through the atmosphere exhaust passage 10 , and enters the atmosphere exhaust port 11 .
It is discharged outside the casing. Among the above atmospheric passages, the part with the highest noise level is the pump storage chamber 7, and the key technical point is how to suppress the noise generated from this storage chamber 7 or prevent it from propagating outside the housing. Since the noise from the blower is small, it will be ignored here and considered as part of the air inflow passage as described above. In order to reduce the noise level in the storage room 7,
Use a low-noise vacuum pump, or
Measures such as installing sound-absorbing material inside the storage chamber 7 have been taken, but such measures alone cannot satisfy the currently required noise level of medical oxygen enrichers, and it is difficult to suppress the propagation of sound from the storage chamber 7. This requires some ingenuity. As a means of achieving this, it is possible to install sound insulating materials in addition to sound absorbing materials inside the storage chamber 7, which can considerably suppress the propagation of sound from the storage chamber 7 through the walls, but the air required to cool the vacuum pump is Due to the large volume, there is a limit to reducing the area of the air inflow opening 8 and the air outflow opening 9, and the leakage of sound from these parts is at a considerably high level, and how to suppress this noise is critical to the entire enrichment device. It affects the height of the noise level. In a membrane type enricher, as shown in Fig. 1, the membrane module 4 etc. are installed in the air inflow path, and the path can also be bent considerably, so that leakage from the air inflow opening 8 is prevented. The noise is considerably attenuated until it reaches the atmosphere intake port 2, and the noise leaking from the atmosphere outflow opening 9 becomes dominant. As a result of intensive studies to suppress the leakage noise to a low level, the inventors of the present invention found that the opening 8 provided in the storage chamber 7
or the passage length from 9 to the opening 2 or 11 of the housing,
That is, if each of the passage lengths 2→8 and 9→11 is made larger than the minimum dimension of the enricher outer shell surface, and the number of passages is bent at least 3 times, leakage noise can be greatly attenuated. It has been found that this can be achieved, and the present invention has been achieved. Generally speaking, the longer the distance through which the atmosphere travels, the lower the noise level will be.However, in the case of noise with a mixture of various frequencies, such as from an enricher, if the distance through which the atmosphere travels is not selected carefully, it will cause resonance. There is a possibility that sound at a specific frequency will be amplified. However, it has been found that by bending the atmospheric passage an appropriate number of times, it is possible to suppress resonance as long as the passage distance is a certain length or more, and at the same time, it is possible to reduce the driving sound of various frequencies almost equally. That is, the passing distance should be at least the minimum value of the outer shell dimension of the enricher, preferably at least 1.5 times. If the passage distance is too short, low frequency sounds will not be attenuated. On the other hand, the sound absorption effect at the bends in the atmospheric passage prevents sound reflection or sound resonance, which has a great effect on noise reduction, but unnecessarily increasing the number of bends complicates the structure of the enricher. Not only does this increase the cost of the housing, but it also increases atmospheric pressure loss and increases the noise level of the blower, which is not desirable. The number of bends is preferably three or more in order to effectively reduce the noise level down to the low frequency range. Furthermore, it is more preferable to install a sound absorbing material or a sound absorbing material and a sound insulating material at the bent portion. Noise countermeasures for general equipment deal with high-frequency noise of around 4000Hz, but oxygen enrichers deal with high-frequency noise of around 100Hz.
The frequency of 2000Hz is dominant, and the above means are very effective in reducing the noise level below 500Hz. FIG. 2 shows various embodiments of atmospheric exhaust passages in membrane enrichers. In Figure 2, the left side of the drawing shows the front side (usually the operating surface) of the enricher, and the part marked with a circle in the middle of the dashed line in the figure represents the essential bending part. show. It is preferable to ignore the bending and exhaustion at the atmosphere exhaust port, as this does not result in a significant reduction in noise. FIG. 2a schematically shows the atmospheric passage in FIG. 1, and the number of bends is 3, and on the sides b, c, and d, the number of bends is 4, 3, and 4, respectively. As shown in FIG. 2c, when the space 14 is formed by the operating side housing wall member 12 and the storage chamber wall member 13, surface noise generated from the periphery of the storage chamber 7 is directly emitted to the outside of the housing. Furthermore, using the space 14 as part of the air path as shown in Figures a and b prevents storage room surface noise and increases the path length and number of bends. It is also very preferable from this point of view. As mentioned above, it is effective to install sound absorbing material at the bend in the air path shown by the dashed line in FIG. It is more preferable to install it at least 1/5 of the total length including the bent part. Adsorption type enrichers do not require a large amount of swept air like the membrane type, but because the pump temperature rises large, they ultimately require the same amount of cooling air as the membrane type. In the adsorption type, since the pump is a compressor, the generated noise is louder than the model, and the structure of the enricher itself is simple, so if the present invention is applied and the cooling air path is devised, the noise level can be significantly reduced. FIG. 3 illustrates an embodiment of the invention. Figure 3a shows an example in which the number of bends in the flow path for atmospheric air to enter and exit the pump storage chamber 7 is 3 times, b and c are 5 times and 4 times, respectively. c indicates the flow path on the outflow side. When b and c are integrated, the part where the passage parts overlap shows a state in which the flow path is divided into two in the direction perpendicular to the plane of the paper, which increases the passage length and the number of bends while simplifying the housing structure. This is an attempt to increase the number of people. e Effects of the Invention According to the present invention, it is possible to attenuate leakage noise from the oxygen enricher and provide an oxygen enricher that can operate extremely quietly. As an example, the noise reduction effect was measured for a membrane type enricher that was bent twice as shown in Figure 4, three times as shown in Figure 2c, and four times as shown in Figure 2b. The results are shown in the table below. In addition, the noise reduction effect is 15 dB to give a sense of quietness.
It is said that (A) or more. 【table】

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明を適用した膜型富化器の概略構
造を、第2図は流出側流路の実施態様の例を、第
3図は吸着型富化器に本発明を適用した実施態様
の例を示し、第4図は本発明の効果を調べるため
屈曲回数を2回とした模型富化器の流出側流路を
示す。
Fig. 1 shows a schematic structure of a membrane enricher to which the present invention is applied, Fig. 2 shows an example of an embodiment of an outflow channel, and Fig. 3 shows an embodiment of an adsorption type enricher to which the present invention is applied. An example of this embodiment is shown in FIG. 4, which shows an outflow channel of a model enricher which was bent twice in order to examine the effects of the present invention.

Claims (1)

【特許請求の範囲】 1 電動機の動力により駆動せめるポンプ手段を
少なくとも1個使用して大気より酸素富化空気を
得る酸素富化器において、該富化器の外殻を形成
する面に設けられた大気取入口及び大気排出口
と、該富化器に内蔵された該電動機及び該ポンプ
手段を収納する室構造であつて該室構造を形成す
る面に設けられた該室構造への大気流入開口部及
び該室構造からの大気流出開口部を有する少なく
とも1個のポンプ収納室と、該大気取入口から該
大気流入開口部への大気の流れを拘束する大気流
入通路と、該大気流出開口部から該大気排出口へ
の大気の流れを拘束する大気排出通路とを有し、
該大気流入通路の長さと該大気排出通路の長さの
各々が該富化器外殻を構成する面における相対す
る両端間の長さの最小値以上であり、該大気流入
通路と該大気排出通路の各々の屈曲回数が3回以
上となるように構成されていることを特徴とする
酸素富化器。 2 該大気流入通路及び/又は該大気排出通路
が、その内面の少なくとも一部に吸音材を設置せ
しめたものである特許請求の範囲第1項記載の酸
素富化器。 3 該大気流入通路及び/又は該大気排出通路
が、その長さの1/5以上の内面に吸音材を設置せ
しめたものである特許請求の範囲第2項記載の酸
素富化器。 4 該大気流入通路及び/又は該大気排出通路
が、少なくとも1ケ所の屈曲部の内面に吸音材を
設置せしめたものである特許請求の範囲第2項記
載の酸素富化器。 5 電動機の動力により駆動せしめるポンプ手段
を少なくとも1個使用して大気より酸素富化空気
を得る酸素富化器において、該富化器の外殻を形
成する面に設けられた大気取入口及び大気排出口
と、該富化器に内蔵された該電動機及び該ポンプ
手段を収納する室構造であつて該室構造を形成す
る面に設けられた該室構造への大気流入開口部及
び該室構造からの大気流出開口部を有する少なく
とも1個のポンプ収納室と、該大気取入口から該
大気流入開口部への大気の流れを拘束する大気流
入通路と、該大気流出開口部から該大気排出口へ
の大気の流れを拘束する大気排出通路とを有し、
該大気流入通路の長さと該大気排出通路の長さの
各々が該富化器外殻を構成する面における相対す
る両端間の長さの最小値以上であり、該大気流入
通路と該大気排出通路の各々の屈曲回数が3回以
上となるように構成され、該富化器の前面側の外
殻の内側の少なくとも一部に空間部を有すること
を特徴とする酸素富化器。 6 該空間部が、該大気流入通路及び/又は該大
気排出通路の一部である特許請求の範囲第5項記
載の酸素富化器。 7 該大気流入通路及び/又は該大気排出通路
が、その内面の少なくとも一部に吸音材を設置せ
しめたものである特許請求の範囲第5項、第6項
いずれかに記載の酸素富化器。
[Scope of Claims] 1. In an oxygen enricher for obtaining oxygen-enriched air from the atmosphere using at least one pump means driven by the power of an electric motor, an oxygen enricher provided on a surface forming an outer shell of the enricher. a chamber structure for accommodating the electric motor and the pump means built in the enricher, and the air inflow into the chamber structure provided on a surface forming the chamber structure; at least one pump housing chamber having an opening and an atmospheric outflow opening from the chamber structure; an atmospheric inflow passage restricting the flow of atmospheric air from the atmospheric intake to the atmospheric inflow opening; and an atmospheric outflow opening. and an atmosphere exhaust passage that restricts the flow of atmosphere from the part to the atmosphere exhaust port,
Each of the length of the atmospheric inflow passage and the length of the atmospheric discharge passage is greater than or equal to the minimum length between opposite ends of the surface constituting the outer shell of the enricher; An oxygen enricher characterized in that each passage is bent three times or more. 2. The oxygen enricher according to claim 1, wherein the atmosphere inlet passage and/or the atmosphere discharge passage has a sound absorbing material installed on at least a part of its inner surface. 3. The oxygen enricher according to claim 2, wherein the atmosphere inlet passage and/or the atmosphere discharge passage has a sound absorbing material installed on the inner surface of 1/5 or more of the length thereof. 4. The oxygen enricher according to claim 2, wherein the atmosphere inflow passage and/or the atmosphere discharge passage has a sound absorbing material installed on the inner surface of at least one bent portion. 5. In an oxygen enricher that obtains oxygen-enriched air from the atmosphere by using at least one pump means driven by the power of an electric motor, an air intake port provided on the surface forming the outer shell of the enricher and an air A chamber structure that houses an exhaust port, the electric motor built in the enricher, and the pump means, an air inflow opening into the chamber structure provided on a surface forming the chamber structure, and the chamber structure. at least one pump housing having an atmospheric outflow opening from the atmospheric outflow opening; an atmospheric inflow passage restricting the flow of atmospheric air from the atmospheric inlet to the atmospheric inflow opening; and from the atmospheric outflow opening to the atmospheric outlet; and an atmospheric exhaust passage that restricts the flow of atmospheric air to the
Each of the length of the atmospheric inflow passage and the length of the atmospheric discharge passage is greater than or equal to the minimum length between opposite ends of the surface constituting the outer shell of the enricher; An oxygen enricher characterized in that each passage is bent three times or more, and has a space at least partially inside an outer shell on the front side of the enricher. 6. The oxygen enricher according to claim 5, wherein the space is a part of the atmosphere inflow passage and/or the atmosphere discharge passage. 7. The oxygen enricher according to any one of claims 5 and 6, wherein the atmosphere inflow passage and/or the atmosphere discharge passage has a sound absorbing material installed on at least a part of its inner surface. .
JP59054405A 1984-03-23 1984-03-23 SANSOFUKAKI Expired - Lifetime JPH0229601B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59054405A JPH0229601B2 (en) 1984-03-23 1984-03-23 SANSOFUKAKI

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59054405A JPH0229601B2 (en) 1984-03-23 1984-03-23 SANSOFUKAKI

Publications (2)

Publication Number Publication Date
JPS60200804A JPS60200804A (en) 1985-10-11
JPH0229601B2 true JPH0229601B2 (en) 1990-07-02

Family

ID=12969783

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59054405A Expired - Lifetime JPH0229601B2 (en) 1984-03-23 1984-03-23 SANSOFUKAKI

Country Status (1)

Country Link
JP (1) JPH0229601B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010120829A (en) * 2008-11-21 2010-06-03 Fukuda Denshi Co Ltd Air feeding device and oxygen concentrator

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61155204A (en) * 1984-12-28 1986-07-14 Teijin Ltd Oxygen enriching apparatus
EP0185980B1 (en) * 1984-12-27 1995-03-01 Teijin Limited Oxygen enriching apparatus
JPS62140619A (en) * 1985-12-12 1987-06-24 Teijin Ltd Oxygen enricher
JP2776992B2 (en) * 1991-01-31 1998-07-16 帝人株式会社 Oxygen concentrator
US7179326B2 (en) 2002-03-05 2007-02-20 Teijin Limited Oxygen concentration apparatus
US7156903B2 (en) * 2003-09-02 2007-01-02 Airsep Corporation Sound enclosure for portable oxygen concentrators

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010120829A (en) * 2008-11-21 2010-06-03 Fukuda Denshi Co Ltd Air feeding device and oxygen concentrator

Also Published As

Publication number Publication date
JPS60200804A (en) 1985-10-11

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